Apparatus and method for recovery and recycle of optical fiber coolant gas

ABSTRACT

An apparatus and method for recovering and recycling a coolant gas from a heat exchanger. The apparatus comprises a coolant gas recovery section, and analysis section, and a coolant gas blending section. The coolant gas recovery section recovers a coolant gas containing contaminants from the heat exchanger. The analysis section monitors a condition of an analysis portion of the recovered coolant gas. The coolant gas blending section operates to produce, based on the condition of the recovered coolant gas monitored by the analysis section, a blend coolant gas comprising a virgin coolant gas and a reclaimed coolant gas that comprises at least a portion of the recovered coolant gas. The blend coolant gas has a predetermined contaminant concentration and is recycled into the heat exchanger. Thus, the coolant gas is recovered from, and recycled to, the heat exchanger at the predetermined contaminant concentration without using a purification device.

BACKGROUND OF THE INVENTION

[0001] 1. Field of the Invention

[0002] The invention generally relates to a coolant recovery andrecycling apparatus. In one aspect, the invention relates to a heliumrecovery and recycling apparatus associated with a heat exchanger.

[0003] 2. Description of the Related Art

[0004] In the production of optical fibers, a glass rod or a “pre-form”,which is especially made to manufacture optical fibers, is processed inan optical fiber drawing system. The optical fiber drawing systemgenerally comprises a furnace, a heat exchanger, a coating applicator, adryer or curing furnace, and a spool as illustrated in European PatentApplication No. 0079188. Initially, the glass rod is melted in thefurnace such that a small, semi-liquid fiber is produced. Thesemi-liquid fiber is then cooled and solidified while falling throughthe air and the heat exchanger. Thereafter, the cooled, solidified fibercan be coated in the coating applicator, dried in the curing furnace ordryer, and drawn with the spool.

[0005] The drawing rate of the optical fiber is generally dependent uponthe cooling rate of the optical fiber in the heat exchanger. That is,the rate at which the fiber can be drawn increases as the rate at whichthe fiber can be cooled increases. To increase the cooling rate of theoptical fiber, a direct heat exchange process is employed. In the directheat exchange process, a coolant gas (e.g., helium, nitrogen, ahelium-nitrogen mixture, a helium-air mixture, a helium-argon mixture, ahelium-hydrogen mixture, a helium-inert gas mixture, and the like) isintroduced into the heat exchanger where the coolant gas directlyencounters and cools the semi-liquid fiber.

[0006] Typically, the heat exchanger comprises a passageway (e.g.,generally of a cylindrical configuration) having end openings (e.g., afiber inlet and a fiber outlet) for receiving and expelling the opticalfiber, one or more coolant gas inlets for receiving the coolant gas, andone or more coolant gas outlets for discharging the coolant gas. Thepassageway generally extends from one end opening proximate a top of theheat exchanger to another end opening proximate a bottom of the heatexchanger. Thus, the passageway provides a corridor through which theoptical fiber can pass. The coolant gas inlet (or inlets) can introducecoolant gas into the passageway while the coolant gas outlet (oroutlets) can remove the coolant gas from the passageway. In aconventional system, a rate of flow of the coolant gas into the heatexchanger is manipulated and/or controlled with metering valves and flowmeters.

[0007] If any of the spent coolant gas is recovered from the heatexchanger, typically proximate the outlet, the recovered coolant gaswill typically be entrained with and/or carry impurities, debris, andthe like (collectively “contaminants”). Typical contaminants includegases (e.g., nitrogen, oxygen, argon, and other gases present in theatmosphere), particulate substances (e.g., dust), and moisture. Thesecontaminants can infiltrate the passageway, coolant gas inlet, and/orcoolant gas outlet of the heat exchanger. The contaminants can collectand increase in concentration in the recovered coolant gas. The amountand/or concentration of contaminants in the recovered coolant gas canlimit and/or restrict the amount of coolant gas that can be recycled andreused.

[0008] In order to reduce the amount and/or concentration ofcontaminants in the recovered coolant gas, a variety of solutions fordecontaminating and/or purifying the coolant gas have been suggested.Coolant gas purification devices, systems, and/or methods are oftenemployed. Such purification devices and/or methods are intended toremove some of the contaminants from the recovered coolant gas so thatat least a portion of the recovered coolant gas can be recycled.However, the use of purification devices can represent a substantialexpense in the optical fiber manufacturing process.

[0009] Unfortunately, without using a purification device, the amount ofimpurities contained within the recovered coolant gas can besubstantial. As attempts are made to recycle more of the recoveredcoolant gas, the contaminant concentration within the recovered coolantgas can resultantly increase. Therefore, a diminishing amount ofrecovered coolant gas can be available for recycling.

[0010] Thus, an efficient and less complex apparatus and method forrecovering and recycling coolant gas would be desirable.

SUMMARY OF THE INVENTION

[0011] In one aspect, the invention provides a method of recovering andrecycling a coolant gas containing contaminants. The method comprisesproviding a heat exchanger and an analyzer, the heat exchanger and theanalyzer in operational association. The coolant gas containingcontaminants is recovered from the heat exchanger and an analysisportion of the recovered coolant gas is delivered to the analyzer.Thereafter, the analysis portion of the recovered coolant gas isanalyzed with the analyzer to determine a condition of the recoveredcoolant gas. Then, based on the condition, a reclaimed portion of therecovered coolant gas is blended with a virgin coolant gas to produce agaseous coolant blend having a predetermined contaminant concentration.The gaseous coolant blend is introduced into the heat exchanger suchthat at least a portion of the recovered coolant gas is recycled.

[0012] In one embodiment, a method of recovering and recycling a coolantgas containing contaminants is employed. The method comprises providinga heat exchanger and an analyzer, the heat exchanger and analyzer inoperational association. The coolant gas containing contaminants isrecovered from the heat exchanger and an analysis portion of therecovered coolant gas is delivered to the analyzer. Thereafter, theanalysis portion of the recovered coolant gas is analyzed with theanalyzer to determine a condition of the recovered coolant gas. Then,based on the condition, a reclaimed portion of the recovered coolant gasis blended with a virgin coolant gas to produce a gaseous coolant blendhaving a predetermined contaminant concentration. The gaseous coolantblend is introduced into the heat exchanger such that at least a portionof the reclaimed recovered coolant gas is recycled. In this embodiment,the reclaimed recovered coolant gas is recycled as opposed to therecovered coolant gas.

[0013] In another embodiment, a method of controlling a contaminantconcentration in a gaseous coolant blend provided to a heat exchanger istaught. The method comprises providing the heat exchanger and ananalyzer, the heat exchanger and the analyzer in operationalassociation. A coolant gas containing contaminants is recovered from theheat exchanger and an analysis portion of the recovered coolant gas isdelivered to the analyzer. Thereafter, the analysis portion of therecovered coolant gas is analyzed with the analyzer to determine thecontaminant concentration within the recovered coolant gas. Then, basedon the contaminant concentration, a reclaimed portion of the recoveredcoolant gas and a virgin coolant gas are blended to produce the gaseouscoolant blend. The reclaimed portion of the recovered coolant gas isrecycled by introducing the gaseous coolant blend into the heatexchanger such that the contaminant concentration in the gaseous coolantblend provided to the heat exchanger is controlled.

[0014] In a further aspect, the invention provides an apparatus for usewith a heat exchanger. The apparatus comprises a coolant recoverysection, an analysis section, and a coolant gas blending section. Thecoolant recovery section is for recovering a coolant gas containingcontaminants from the heat exchanger. The analysis section is operableto monitor a condition of the recovered coolant gas. The coolant gasblending section, in operational association with the coolant gasrecovery section and the analysis section, is operable to produce, basedon the condition of the recovered coolant gas, a gaseous coolant blendhaving a predetermined contaminant concentration from a virgin coolantgas and a reclaimed portion of the recovered coolant gas.

[0015] In one embodiment, an apparatus for recovering a coolant gascontaining contaminants from a heat exchanger and recycling at least aportion of the recovered coolant gas is disclosed. The apparatuscomprises a pump operable to recover the coolant gas from the heatexchanger and to transport the recovered coolant gas through theapparatus and an analyzer operable to monitor a condition of therecovered coolant gas. The apparatus also comprises a first mass flowcontroller operable to reclaim a portion of the recovered coolant gas bydelivering the reclaimed portion of the recovered coolant gas to amixing point, a second mass flow controller operable to provide a virgincoolant gas to the mixing point, and a third mass flow controlleroperable to maintain a flow of the recovered coolant gas through theapparatus. As such, the apparatus is operable to produce, based on thecondition of the recovered coolant gas, a gaseous coolant blend from thevirgin coolant gas and the reclaimed portion of the recovered coolantgas. Thus, the gaseous coolant blend has a predetermined contaminantconcentration when the gaseous coolant blend is introduced into the heatexchanger.

[0016] In yet another aspect, the invention provides a coolant gasrecovery system that comprises a coolant gas for cooling a hot fiber, aheat exchanger, a pump for pumping and drawing the coolant gas throughthe system, an analyzer for monitoring an impurity concentration in thecoolant gas, a first mass flow controller and a second mass flowcontroller for controlling the impurity concentration in the coolant gasbased on the monitored impurity concentration, and a third mass flowcontroller for providing a seal to the heat exchanger using the coolantgas and for maintaining a constant flow of the coolant gas to ensurecontinuous operation of the pump.

[0017] The heat exchanger includes a fiber inlet, a fiber outlet, apassageway, one or more coolant gas inlets, and one or more coolant gasoutlets. The fiber inlet is adapted to receive the hot fiber into theheat exchanger and the fiber outlet is adapted to expel the hot fiberfrom the heat exchanger. The passageway extends between the fiber inletand fiber outlet and is adapted to pass therethrough the hot fiber. Thecoolant gas inlets are for introducing a coolant gas into the passagewayand the coolant gas outlets are for removing the coolant gas from thepassageway.

BRIEF DESCRIPTION OF THE DRAWINGS

[0018] Embodiments of the invention are disclosed with reference to theaccompanying drawings and are for illustrative purposes only. Theinvention is not limited in its application to the details ofconstruction, or the arrangement of the components, illustrated in thedrawings. The invention is capable of other embodiments or of beingpracticed or carried out in other various ways. Like reference numeralsare used to indicate like components throughout the drawings.

[0019]FIG. 1 illustrates a schematic flow diagram of an embodiment of acoolant gas recovery and recycling system according to one aspect of theinvention.

[0020]FIG. 2 illustrates a heat exchanger that can be employed withinthe system of FIG. 1.

[0021]FIG. 3 illustrates a chart detailing the optimum flow of recycledcoolant gas that achieves maximum cooling gas recovery while minimizingthe contaminants in the recovered coolant gas using the system of FIG.1.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0022] Various items of equipment, such as fittings, valves, mountings,pipes, wiring, and the like have been omitted to simplify thedescription. However, such conventional equipment and its uses are knownto those skilled in the art and can be employed as desired. Moreover,although the present invention is described below in the context ofrecovering and recycling a coolant gas, the invention can be employedwith, and has applicability to, many different recovery and/or recyclingapparatuses and processes.

[0023] Referring to FIG. 1, a system 10 for recovering and recycling acoolant gas, such as helium, nitrogen, a helium-nitrogen mixture, ahelium-air mixture, and the like is shown. System 10 comprises heatexchanger 12, coolant gas recovery section 14, analysis section 16, andcoolant gas blending section 18, which are in operational associationwith each other.

[0024] Heat exchanger 12, as shown in detail in FIG. 2, can include avariety of heat exchangers (e.g., direct heat exchanging or likedevices) known in the art that are capable of accepting, receiving,and/or processing a hot optical fiber, a semi-liquid fiber, and thelike. As shown in FIG. 2, heat exchanger 12 comprises coolant gas inlet20, coolant gas outlet 22, passageway 24, and end openings 26 (e.g., afiber inlet and a fiber outlet). While heat exchanger 12 can include oneor more coolant gas inlets 20 and one or more coolant gas outlets 22,for purposes of illustration, only a single coolant gas inlet and asingle coolant gas outlet are shown in FIG. 2.

[0025] Coolant gas inlet 20 is configured to accept delivery and/orintroduction of coolant gas into heat exchanger 12 while coolant gasoutlet 22 is configured to remove, expel, and/or permit recovery of thecoolant gas from the heat exchanger. Passageway 24 can be formed throughheat exchanger 12 and extend between end openings 26 at opposing ends 28of the heat exchanger. End openings 26 are structured to receive anddischarge the hot optical fiber from heat exchanger 12. Therefore,passageway 24 and end openings 26 provide the hot optical fiber with apath, corridor, and/or route in which to pass through heat exchanger 12.Thus, the coolant gas can be introduced into heat exchanger 12 atcoolant gas inlet 20, can flow through or circulate throughoutpassageway 24, and can cool the hot optical fiber. Thereafter, thecoolant gas can be removed, drawn, and/or recovered from the heatexchanger at coolant gas outlet 22.

[0026] Often, coolant gas that is recovered from heat exchanger 12contains contaminants such as impurities, debris, and the like,(collectively “contaminants”). These contaminants typically comprisegases (e.g., nitrogen, oxygen, argon, and other gases present in theatmosphere), particulate substances (e.g., dust), and moisture. However,contaminants can include any substance other than the coolant gas andcan exist within the recovered coolant gas in varying amounts and atvarying concentrations.

[0027] In contrast to recovered coolant gas, “virgin” coolant gas iscoolant gas that contains little, if any, contaminants. Virgin coolantgas such as, for example, an industrial grade virgin coolant gas,typically contains no more than about 0.005 percent contaminants byvolume.

[0028] Referring back to FIG. 1, coolant gas recovery section 14includes pump 30, recovery lines 32, and optionally orifice 34 or a likede-coupling device and/or flow restrictor. Pump 30 is operable toproduce both a negative and a positive pressure within system 10. Forexample, pump 30 can produce or create the negative pressure in recoverylines 32 a and 32 b such that the coolant gas within heat exchanger 12can be drawn from the heat exchanger and recovered. Also, pump 30 canproduce or create positive pressure in one or more lines (i.e., 32 c, 32d, and 32 e) and elsewhere within system 10, such that the coolant gascan be pushed or flowed throughout the system. Any pump capable ofproducing the negative and/or positive pressures described above can beemployed as pump 30.

[0029] Since pump 30 is operable to generate both negative and positivepressures, additional pumps, a compressor, and the like are not neededwithin system 10. The level and/or amount of positive pressure generatedby pump 30 can be dependent upon the amount of the coolant gas flowingthrough system 10 and/or flow restrictions provided by components of thesystem.

[0030] Orifice 34 is disposed within system 10, and coolant gas recoverysection 14, such that the orifice can de-couple heat exchanger 12 frompump 30. Orifice 34 is also capable of controlling and/or reducing theeffects of pressure differentials within heat exchanger 12. Thesepressure differentials are created by pump 30 as the pump operates toproduce both positive and negative pressures within system 10. If notcontrolled, the pressure differentials (i.e., fluctuations in pressure)can produce undesirable fiber vibrations. Undesirable fiber vibrationscan adversely affect the fiber-drawing process and the quality of theoptical fiber that is produced.

[0031] Analysis section 16 includes an analyzer 36 and analysis line 38.Analyzer 36 can comprise one or more of a variety of analyzers ormonitors known in the art such as, for example, an oxygen analyzer, ahelium analyzer, a nitrogen analyzer, a moisture analyzer, and the like.Analyzer 36 can be associated, though recovery lines 32 and analysisline 38, with heat exchanger 12 such that the analyzer is operable tomonitor a condition of the recovered coolant gas (or an analysis portionof the recovered coolant gas) drawn from the heat exchanger. Conditionsof the recovered coolant gas that can be monitored include, but are notlimited to, an amount and/or concentration of oxygen, an amount and/orconcentration of helium, an amount and/or concentration of nitrogen, anamount and/or concentration of another inert gas, and an amount ofmoisture in the recovered coolant gas.

[0032] Preferably, analyzer 36 is operationally associated with acontrol system 37. Control system 37 is operable to relay and/ortransmit the condition monitored by the analyzer to one or morecomponents of system 10 (e.g., mass flow controllers, flow controllers,valves, and the like). Control system 37 can further operate to instructand/or control one or more mass flow controllers, based on themonitored, relayed, and/or transmitted condition, regarding flow ratesand other operational parameters.

[0033] Coolant gas blending section 18 includes flow or mass flowcontrollers 40 and 42, virgin line 44, reclaimed line 46, and blend line48. Mass flow controller 40 is operable to permit or restrict a flow ofthe recovered coolant gas. Specifically, the recovered coolant gas canbe selectively permitted to pass through mass flow controller 40 andinto reclaimed line 46 whereby the recovered coolant gas is “reclaimed”.The reclaimed coolant gas can then flow through reclaimed line 46 tomixing point 50.

[0034] Mass flow controller 42 is operable to permit or restrict a flowof the virgin coolant gas. Specifically, the virgin coolant gas can bepermitted to pass through mass flow controller 42 and into virgin line44. The virgin coolant gas can then flow through virgin line 44 tomixing point 50.

[0035] Mixing point 50, as shown in FIG. 1, occurs at the intersectionof virgin line 44, reclaimed line 46, and blend line 48. At mixing point50, the reclaimed coolant gas and the virgin coolant gas can be blendedtogether to produce a mixture and/or blend of coolant gas at apredetermined and/or desired purity. In other words, the blend ofcoolant gas can be produced such that the blend has a predetermined,known, and/or desired contaminant concentration (collectively“predetermined contaminant concentration”).

[0036] Typically, the predetermined contaminant concentration of theblend coolant gas is less than about five percent (5%) contaminants byvolume of the blend coolant gas. Correspondingly, the coolant gasrecycled by system 10 has a coolant gas concentration (i.e., purity) ofabout ninety-five to about ninety-nine percent (about 95 to about 99%)coolant gas by volume of the blend coolant gas. In preferredembodiments, the predetermined contaminant concentration and the coolantgas concentration in the blend coolant gas can be user defined.

[0037] In one embodiment, the predetermined contaminant concentrationcan be achieved by selectively operating mass flow controllers 40 and 42to blend varying amounts of reclaimed coolant gas and virgin coolant gastogether in an appropriate proportion. The blend coolant gas can beproduced using this “blending” method since the contaminantconcentration within the virgin coolant gas is generally known and theanalyzer can determine the contaminant concentration within therecovered coolant gas.

[0038] Once the blend coolant gas is produced at mixing point 50, theblend coolant gas is passed through blend line 48 for introduction intoheat exchanger 12. As such, the blend coolant gas, and more specificallythe reclaimed portion of the recovered coolant gas, is “recycled”. Theheat exchanger can use the recycled coolant gas to cool a hot opticalfiber as previously described and, since the blend coolant gas, whichincludes the reclaimed portion of the recovered coolant gas, is recycledand/or reused, a significant cost savings can be realized.

[0039] In preferred embodiments, system 10 also includes by-pass section52. By-pass section 52 includes mass flow controller 54 and one or moreseal lines 56 a-b. Mass flow controller 54 is operable to permit orrestrict a flow of the recovered coolant gas through seal line 56 a. Therecovered coolant gas can flow through analyzer 36, analysis line 38,and seal lines 56 a-b until passing proximate ends 28 of heat exchanger12 such that seals 58 a-b are formed. Seals 58 a-b can comprise, forexample, a conventional gas seal. Thus, by-pass section 52 can inhibitand/or prevent undesirable escape of the coolant gas from withinpassageway 24 of heat exchanger 12 and, in doing so, utilize a portionof the recovered coolant gas.

[0040] In an exemplary embodiment, seals 58 a-b comprise seals such asthose described in commonly-owned, co-pending U.S. patent applicationSer. No. 09/998,288 filed Nov. 30, 2001, entitled “Cap Assembly andOptical Fiber Cooling Process” and, therefore, the contents anddisclosure of that application are incorporated into the presentapplication by this reference as if fully set forth herein.

[0041] Further, by-pass section 52, and particularly mass flowcontroller 54, can operate to maintain a constant flow of at least aportion of the recovered coolant gas through system 10. The constantflow can resultantly ensure that pump 30 continually operates. With acontinually operating pump 30, positive pressure generated by the pump,which transports the recovered, reclaimed, and blended coolant gasthrough system 10, can be maintained. By maintaining the positivepressure in system 10, “lag time” can be reduced. As used herein, lagtime is essentially that amount of time that elapses while the recoveredcoolant gas progresses through system 10 (e.g., through lines 32 d and38 to reach analyzer 36).

[0042] Lag time is often undesirably noticed and/or experienced whendiverting and/or redirecting flows of the coolant gas from line to line(e.g., 56 and 46) within system 10. For example, when mass flowcontroller 54 restricts the flow of a portion of the recovered coolantgas entering seal line 56 a, and mass flow controller 40 simultaneouslypermits an increased flow of a portion of the recovered coolant gasthrough reclaimed line 46, lag time might be expected. However, becausepump 30 has been continually operating, a build-up of positive pressureis not necessary to divert and/or redirect the recovered coolant gas.Therefore, the portion of the recovered coolant gas that had beenentering seal line 56 a can be quickly diverted to reclaimed line 46.When positive pressure within system 10 is not allowed to substantiallydissipate as a result of the continuously and/or continually operatingpump, lag time can be reduced.

[0043] Advantageously, by-pass section 52 can also inhibit and/orprevent accumulation of contaminants upstream of mass flow controller 40that are caused by a decreasing flow of recovered coolant gas at anincreasing concentration of the recovered coolant gas.

[0044] In operation, a coolant gas having contaminants is drawn (i.e.,recovered) from heat exchanger 12 by operating pump 30. The recoveredcoolant gas enters recovery line 32 a and flows through orifice 34,recovery line 32 b, pump 30, and recovery line 32 c. While progressingthrough recovery line 32 c, the coolant gas having contaminants isdivided and/or splits such that at least a portion of the recoveredcoolant gas flows through recovery line 32 d and another portion flowsthrough recovery line 32 e.

[0045] Of the portion of the recovered coolant gas flowing throughrecovery line 32 d, an analysis portion enters analysis line 38 and isintroduced into analyzer 36 and a portion passes through mass flowcontroller 54. Preferably, the flow of the portions of recovered coolantgas through each of analyzer 36 and mass flow controller 54 are constantor substantially constant while the flow of recovered coolant gasthrough recovery line 32 e and mass flow controller 40 is variable.

[0046] Positive pressure generated by pump 30 can be directly relatedand/or depend upon a combination of the flows of recovered coolant gasthrough analyzer 36 and mass flow controllers 40 and 54. In other words,pump 30 can operate to produce as much or as little positive pressure asneeded depending on a summation of flow restrictions produced byanalyzer 36 and mass flow controllers 40 and 54.

[0047] After the recovered coolant gas has been divided, analyzer 36operates to monitor a condition of the analysis portion of the recoveredcoolant gas and, as such, can determine the contaminant concentrationwithin the recovered coolant gas. Thereafter, analyzer 36 and/or controlsystem 37 transmits and/or relays the concentration information to oneor more of mass flow controllers 40, 42, and 54. Analyzer 36 and/orcontrol system 37 can also, if desired, instruct and/or control one ormore of mass flow controllers 40, 42, and 54 to manipulate flows of therecovered coolant gas.

[0048] Having determined the contaminant concentration of the recoveredcoolant gas with analyzer 36, and knowing the contaminant concentrationwithin the virgin coolant gas, mass flow controller 40 and 42 areactuated and/or operated. When mass flow controller 42 is actuated, anamount of the virgin coolant gas travels through virgin line 44 and isdelivered to mixing point 50. Also, when mass flow controller 40 isactuated, an amount of recovered coolant gas is permitted to passthrough the mass flow controller such that the amount of the recoveredcoolant gas is reclaimed. The reclaimed coolant gas travels throughreclaimed line 46 and is also delivered to mixing point 50.

[0049] At mixing point 50, the reclaimed coolant gas and the virgincoolant gas are blended and/or mixed together to produce the blendcoolant gas (i.e., gaseous coolant blend) having the predeterminedcontaminant concentration or coolant gas purity. Thus, the quality ofthe coolant gas (i.e., the contaminant concentration or purity), asopposed to quantity (i.e., rate of flow) of the coolant gas, ismanipulated and/or controlled by system 10, and particularly mass flowcontrollers 40 and 42.

[0050] After the blend coolant gas, at the predetermined concentration,has been produced, the blend coolant gas is passed through blend line 48until entering heat exchanger 12 under the positive pressure of pump 30.As such, the blend coolant gas, and specifically the recovered coolantgas that was reclaimed, is “recycled” by once again using or employingthe blend coolant gas and/or the recovered coolant gas within heatexchanger 12 to cool the optical fiber.

[0051] When coolant gas is recycled using system 10, the concentrationof the blend coolant gas can be predetermined and the flow rate of theblend coolant gas into heat exchanger 12 can remain substantiallyconstant. For example, if the recovered coolant gas contains arelatively high contaminant concentration, then less of the recoveredcoolant gas and more of the virgin coolant gas are blended together toproduce the mixture possessing the desired level of contaminants.Conversely, if the recovered coolant gas contains a relatively lowcontaminant concentration, then more of the recovered coolant gas andless of the virgin coolant gas are blended together to produce themixture possessing the desired level of contaminants.

[0052] Additionally, because the steps of recovering and reclaimingcoolant gas can be performed repeatedly within system 10, it isimportant to note that the lower the flow of reclaimed coolant gas thelower the contaminant concentration that will be entrained in therecovered coolant gas.

[0053] Also, no matter what the ratio of reclaimed coolant gas to virgincoolant gas may be when the blend coolant gas having the predeterminedcontaminant concentration is produced, the flow rate of the blendcoolant gas into heat exchanger 12 can stay the same or substantiallythe same. Thus, the flow rate of the blend coolant gas into heatexchanger 12 does not depend upon the contaminant concentration in therecovered or reclaimed coolant gas.

[0054] Preferably, the amount of recovered coolant gas that is reclaimedand used to produce the blended coolant gas is optimized to ensure thatthe maximum amount of recovered coolant gas is reclaimed and thenrecycled. In one embodiment, optimization can be achieved by solving asystem of flow and concentration equations. Such optimization, withreference to FIG. 1, is described below.

[0055] First, the impurity concentration of the recovered coolant gas,y_(r), is determined by analyzer 36. Then, mass flow controller 42receives the virgin coolant gas flowing at f_(v) and having impurityconcentration y_(v) and mass flow controller 40 receives the recoveredcoolant gas flowing at f_(r) and having impurity concentration y_(r).Blending section 18 operates such that the blended coolant gas havingflow f_(p) with impurity y_(p) is produced. The blended coolant gas flowf_(p) can be determined by:

f _(p) =f _(v) +f _(r)  (1)

[0056] while the impurity concentration y_(p) of the blended coolant gasis governed by:

y _(p) f _(p) =y _(v) f _(v) +y _(r) f _(r)  (2)

[0057] Having or knowing desired values for f_(p) and y_(p),ascertaining Y_(r) with analyzer 36, and knowing the impurityconcentration within virgin coolant gas y_(V), both f_(r) and f_(v) canbe solved for using the blended coolant gas flow and impurityconcentration equations (1) and (2). As a result, f_(p) at a desiredconcentration y_(p) can be achieved by manipulating the recoveredcoolant gas flow f_(r) and virgin coolant gas flow f_(v) according tothe equations: $\begin{matrix}{{f_{r}\left( y_{r} \right)} = {f_{p}\frac{y_{p} - y_{v}}{y_{r} - y_{v}}}} \\{{f_{v}\left( y_{r} \right)} = {f_{p}\frac{y_{r} - y_{p}}{y_{r} - y_{v}}}}\end{matrix}$

[0058] Since the impurity concentration of the recovered coolant gasy_(r) was found to be dependent upon suction flow f_(s) in recovery line32 a when f_(s) is less than f_(r), the y_(r) dependence on f_(s) can bedirectly determined by introducing virgin coolant gas that is 100% pure(e.g., substantially free of or lacking contaminants) into heatexchanger 12 such that:

y _(p) =y _(v)=0

[0059] The resulting impurity concentration of the recovered coolant gasY_(r) can then be measured for varying f_(s) values such that:

y _(r) ⁰ =y _(r) ⁰(f _(s))

[0060] Then, the impurity concentration of the recovered coolant gasy_(r) fulfills:

y _(r)(f _(s))=y _(p)+(1−y _(p))y _(r) ⁰(f _(s))

[0061] Referring to FIG. 3, the dependencies Y_(r) (f_(s)) and f_(r)(y_(r)) are illustrated. At the maximum recovery rate, each equation:

y _(r)(f _(s))=y _(p)+(1−y _(p))y _(r) ⁰(f _(s))${f_{r}\left( y_{r} \right)} = {f_{p}\frac{y_{p} - y_{v}}{y_{r} - y_{v}}}$

[0062] is fulfilled and, therefore, the optimum recovered gas flow,f_(r) ^(opt), with the impurity concentration, y_(r) ^(opt), occurs atthe intersection point of the two curves produced when the aboveequations are solved. Thus, the optimum recovered gas flow at theoptimum concentration can be achieved.

[0063] When employed, system 10 can provide numerous advantages. Forexample, system 10 can continually maintain an increased or elevatedrate of coolant gas recovery and can reduce contamination in therecovered coolant gas by reducing suction flow. Further, system 10 caninsure and/or promote a constant flow of coolant gas, f_(p), at aconstant concentration. In other words, there is typically no “toggling”between only virgin gas and blended gas. Additionally, the use of system10 can avoid the need for a variable speed pump, blower, or other meansfor controlling suction pressure. System 10 does not require coolant gasventing in order to control the fiber-cooling process and no pressure orvacuum measurements need to be taken. Notably, each of these advantagesis accomplished without unnecessary or extraneous equipment added to, oremployed within, system 10.

[0064] Despite any methods being outlined in a step-by-step sequence,the completion of acts or steps in a particular chronological order isnot mandatory. Further, elimination, modification, rearrangement,combination, reordering, or the like, of acts or steps is contemplatedand considered within the scope of the description and appended claims.

[0065] While the present invention has been described in terms of thepreferred embodiment, it is recognized that equivalents, alternatives,and modifications, aside from those expressly stated, are possible andwithin the scope of the appended claims.

What is claimed is:
 1. A method of recovering and recycling a coolantgas containing contaminants, the method comprising: providing a heatexchanger and an analyzer, the heat exchanger and the analyzer inoperational association; recovering the coolant gas containingcontaminants from the heat exchanger; delivering an analysis portion ofthe recovered coolant gas to the analyzer; analyzing the analysisportion of the recovered coolant gas with the analyzer to determine acondition of the recovered coolant gas; blending, based on thecondition, a reclaimed portion of the recovered coolant gas and a virgincoolant gas to produce a gaseous coolant blend having a predeterminedcontaminant concentration; and introducing the gaseous coolant blendinto the heat exchanger such that at least a portion of the recoveredcoolant gas is recycled.
 2. The method of claim 1, wherein the methodfurther comprises a step of introducing the virgin coolant gas into theheat exchanger prior to the recovering step.
 3. The method of claim 1,wherein the recovering step and the delivering step are performed by asingle pump.
 4. The method of claim 1, wherein the method furthercomprises providing the analysis portion of the recovered coolant gas toa seal associated with the heat exchanger.
 5. The method of claim 1,wherein the method further comprises providing a seal for the heatexchanger using the recovered coolant gas.
 6. The method of claim 1,wherein the method further comprises providing a control system, thecontrol system associated with the analyzer and operable to control theblending.
 7. The method of claim 1, wherein the analysis portion of therecovered coolant gas passes through the analyzer at a constant rate offlow.
 8. The method of claim 1, wherein the gaseous coolant blend isintroduced into the heat exchanger at a constant rate of flow.
 9. Themethod of claim 1, wherein the method further comprises providing meansfor controlling an amount of contaminants introduced into the heatexchanger.
 10. The method of claim 1, wherein the method furthercomprises providing means for controlling a contaminant concentration inthe gaseous coolant blend.
 11. The method of claim 1, wherein the methodfurther comprises providing means for controlling a contaminantconcentration in the gaseous coolant blend introduced into the heatexchanger.
 12. The method of claim 1, wherein the method furthercomprises dividing the recovered coolant gas into a portion of therecovered coolant gas that includes the analysis portion of therecovered coolant gas and the reclaimed portion of the recovered coolantgas.
 13. The method of claim 1, wherein the predetermined contaminantconcentration of the gaseous coolant blend is user defined.
 14. Themethod of claim 1, wherein the method further comprises maintaining aflow of a portion of the recovered coolant gas through a by-passsection.
 15. The method of claim 14, wherein the method furthercomprises simultaneously decreasing the flow of the portion of therecovered coolant gas through the by-pass section and increasing theflow of the reclaimed coolant gas through the blending section.
 16. Themethod of claim 14, wherein the maintaining the flow of the portion ofthe recovered coolant gas through the by-pass section reduces lag time.17. A method of recovering and recycling a coolant gas containingcontaminants, the method comprising: providing a heat exchanger and ananalyzer, the heat exchanger and analyzer in operational association;recovering the coolant gas containing contaminants from the heatexchanger; delivering an analysis portion of the recovered coolant gasto the analyzer; analyzing the analysis portion of the recovered coolantgas with the analyzer to determine a condition of the recovered coolantgas; blending, based on the condition, a reclaimed portion of therecovered coolant gas and a virgin coolant gas to produce a gaseouscoolant blend having a predetermined contaminant concentration; andintroducing the gaseous coolant blend into the heat exchanger such thatat least a portion of the reclaimed recovered coolant gas is recycled.18. A method of controlling a contaminant concentration in a gaseouscoolant blend provided to a heat exchanger, the method comprising:providing the heat exchanger and an analyzer, the heat exchanger and theanalyzer in operational association; recovering a coolant gas containingcontaminants from the heat exchanger; delivering an analysis portion ofthe recovered coolant gas to the analyzer; analyzing the analysisportion of the recovered coolant gas with the analyzer to determine thecontaminant concentration within the recovered coolant gas; andblending, based on the contaminant concentration, a reclaimed portion ofthe recovered coolant gas and a virgin coolant gas to produce thegaseous coolant blend; recycling the reclaimed portion of the recoveredcoolant gas by introducing the gaseous coolant blend into the heatexchanger such that the contaminant concentration in the gaseous coolantblend provided to the heat exchanger is controlled.
 19. The method ofclaim 18, wherein the method further comprises introducing a portion ofthe recovered coolant gas into a by-pass section, the by-pass sectionproviding a seal to the heat exchanger and ensuring continuous operationof a pump.
 20. An apparatus for use with a heat exchanger, the apparatuscomprising: a coolant recovery section for recovering a coolant gascontaining contaminants from the heat exchanger; an analysis sectionoperable to monitor a condition of the recovered coolant gas; and acoolant gas blending section in operational association with the coolantgas recovery section and the analysis section, the coolant gas blendingsection operable to produce, based on the condition of the recoveredcoolant gas, a gaseous coolant blend having a predetermined contaminantconcentration from a virgin coolant gas and a reclaimed portion of therecovered coolant gas.
 21. The apparatus of claim 20, wherein thecoolant gas recovery section comprises a pump operable to produce both anegative pressure and a positive pressure within the apparatus.
 22. Theapparatus of claim 20, wherein the coolant gas recovery sectioncomprises an orifice capable of reducing, within the heat exchanger, theeffects of pressure differentials created by the pump.
 23. The apparatusof claim 20, wherein the coolant gas blending section comprises a meansfor controlling flow.
 24. The apparatus of claim 23, wherein the meansfor controlling flow is selected from the group consisting of a firstand second flow controller, a first and second mass flow controller, anda first and second valve.
 25. The apparatus of claim 20, wherein thevirgin coolant gas contains less than about 0.005 percent contaminantsby volume of the virgin coolant gas.
 26. The apparatus of claim 20,wherein the predetermined concentration of the contaminants is less thanabout 5 percent contaminants by volume of the gaseous coolant blend. 27.The apparatus of claim 20, wherein the condition is selected from thegroup consisting of an amount of moisture, a concentration of oxygen,and a concentration of an inert gas in the recovered coolant gas. 28.The apparatus of claim 20, wherein the analysis section includes ananalyzer selected from the group consisting of an oxygen analyzer, aninert gas analyzer, and a moisture analyzer.
 29. The apparatus of claim20, wherein the apparatus further comprises a by-pass section forproviding a gas seal to the heat exchanger.
 30. The apparatus of claim29, wherein the by-pass section utilizes at least a portion of therecovered coolant gas to provide the gas seal.
 31. An apparatus forrecovering a coolant gas containing contaminants from a heat exchangerand recycling at least a portion of the recovered coolant gas, theapparatus comprising: a pump operable to recover the coolant gas fromthe heat exchanger and to transport the recovered coolant gas throughthe apparatus; an analyzer operable to monitor a condition of therecovered coolant gas; a first mass flow controller operable to reclaima portion of the recovered coolant gas by delivering the reclaimedportion of the recovered coolant gas to a mixing point; a second massflow controller operable to provide a virgin coolant gas to the mixingpoint; a third mass flow controller operable to maintain a flow of therecovered coolant gas through the apparatus; wherein the apparatus isoperable to produce, based on the condition of the recovered coolantgas, a gaseous coolant blend from the virgin coolant gas and thereclaimed portion of the recovered coolant gas such that the gaseouscoolant blend has a predetermined contaminant concentration when thegaseous coolant blend is introduced into the heat exchanger.
 32. Theapparatus of claim 31, wherein a combined flow of recovered coolant gasthrough the first mass flow controller, the third mass flow controller,and the analyzer determine a pressure generated by the pump fortransporting the recovered coolant gas.
 33. The apparatus of claim 31,wherein a flow of the recovered coolant gas passing through the analyzeris constant.
 34. The apparatus of claim 31, wherein the flow of therecovered coolant gas through the third mass flow controller isrestricted while the flow of the recovered coolant gas through the firstmass flow controller is simultaneously increased.
 35. The apparatus ofclaim 31, wherein the apparatus further comprises a control systemassociated with the analyzer and capable of actuating the first massflow controller, the second mass flow controller, and the third massflow controller based on the condition of the recovered coolant gas. 36.The apparatus of claim 31, wherein the apparatus further comprises acontrol system associated with the analyzer and capable of actuating thefirst mass flow controller and the second mass flow controller toproduce the gaseous coolant blend at the predetermined concentration.37. The apparatus of claim 31, wherein the apparatus further comprisesan orifice for de-coupling the pump and the heat exchanger and reducing,within the heat exchanger, pressure differential effects produced by thepump.
 38. A coolant gas recovery system comprising: a coolant gas forcooling a hot fiber; a heat exchanger including: a fiber inlet adaptedto receive the hot fiber into the heat exchanger; a fiber outlet adaptedto expel the hot fiber from the heat exchanger; a passageway extendingbetween the fiber inlet and fiber outlet, the passageway adapted to passtherethrough the hot fiber; one or more coolant gas inlets forintroducing a coolant gas into the passageway; and one or more coolantgas outlets for removing the coolant gas from the passageway; a pump forpumping and drawing the coolant gas through the system; an analyzer formonitoring an impurity concentration in the coolant gas; a first massflow controller and a second mass flow controller for controlling theimpurity concentration in the coolant gas based on the monitoredimpurity concentration; and a third mass flow controller for providing aseal to the heat exchanger using the coolant gas and for maintaining aconstant flow of the coolant gas to ensure continuous operation of thepump.
 39. The system of claim 38, wherein the coolant gas is selectedfrom the group consisting of helium, nitrogen, a helium-nitrogenmixture, and a helium-air mixture.